Engineering and therapeutic application of single-chain bivalent TGF-ß family traps.

Deregulation of TGF-ß superfamily signaling is a causative factor in many diseases. Here we describe a protein engineering strategy for the generation of single-chain bivalent receptor traps for TGF-ß superfamily ligands. Traps were assembled using the intrinsically disordered regions flanking the structured binding domain of each receptor as "native linkers" between two binding domains. This yields traps that are approximately threefold smaller than antibodies and consists entirely of native receptor sequences. Two TGF-ß type II receptor-based, single-chain traps were designed, termed (TßRII)2 and (TßRIIb)2, that have native linker lengths of 35 and 60 amino acids, respectively. Both single-chain traps exhibit a 100 to 1,000 fold higher in vitro ligand binding and neutralization activity compared with the monovalent ectodomain (TßRII-ED), and a similar or slightly better potency than pan-TGF-ß-neutralizing antibody 1D11 or an Fc-fused receptor trap (TßRII-Fc). Despite its short in vivo half-life (<1 hour), which is primarily due to kidney clearance, daily injections of the (TßRII)2 trap reduced the growth of 4T1 tumors in BALB/c mice by 50%, an efficacy that is comparable with 1D11 (dosed thrice weekly). In addition, (TßRII)2 treatment of mice with established 4T1 tumors (100 mm(3)) significantly inhibited further tumor growth, whereas the 1D11 antibody did not. Overall, our results indicate that our rationally designed bivalent, single-chain traps have promising therapeutic potential.

A simplified polyethylenimine-mediated transfection process for large-scale and high-throughput applications.

Transient gene expression in mammalian cells is a valuable alternative to stable cell lines for the rapid production of large amounts of recombinant proteins. While the establishment of stable cell lines takes 2-6 months, milligram amounts of protein can be obtained within a week following transfection. The polycation polyethylenimine (PEI) is one of the most utilized reagents for small- to large-scale transfections as it is simple to use and, when combined with optimized expression vectors and cell lines, provides high transfection efficiency and titers. As with most transfection reagents, PEI-mediated transfection involves the formation of nanoparticles (polyplexes) which are obtained by its mixing with plasmid DNA. A short incubation period that allows polyplexes to reach their optimal size is performed prior to their addition to the culture. As the quality of polyplexes directly impacts transfection efficiency and productivity, their formation complicates scalability and automation of the process, especially when performed in large-scale bioreactors or small-scale high-throughput formats. To avoid variations in transfection efficiency and productivity that arise from polyplexes formation step, we have optimized the conditions for their creation directly in the culture by the consecutive addition of DNA and PEI. This simplified approach is directly transferable from suspension cultures grown in 6-well plates to shaker flasks and 5-L WAVE bioreactors. As it minimizes the number of steps and does not require an incubation period for polyplex formation, it is also suitable for automation using static cultures in 96-well plates. This "direct" transfection method thus provides a robust platform for both high-throughput expression and large-scale production of recombinant proteins.

Noninvasive probing of inhibitory effects of cylindrospermopsin and microcystin-LR using cell-based impedance spectroscopy.

In an effort to develop a noninvasive method for assessment of cyanobacterial toxins in drinking water, plausible cytotoxicity/inhibition of microcystin-LR and cylindrospermopsin was evaluated by cell-substrate impedance sensing (ECIS) using three different cell lines. Sf9 insect cells were attached to concanavalin A coated gold electrodes, whereas Chinese hamster ovary (CHO) and human embryo kidney (HEK) cells were attached to a fibronectin or laminin coated gold surface. Cytotoxic or inhibitory effects were dependent upon the cell line and the extracellular matrix (ECM) coating. Neither toxin exhibited any appreciable effect on the insect cells. In contrast, cytotoxicity of cylindrospermopsin on CHO cells was attested by both ECIS and viability tests. The half-inhibition concentration (ECIS50) of cylindrospermopsin for CHO cells was approximately 2 microg/mL (ppm) after 20 h of exposure and 4 microg/mL (ppm) after 30 h of exposure for a laminin or fibronectin coated surface. ECIS confirmed no significant effect of cylindrospermopsin on HEK cells. Microcystin-LR was also tested with CHO cells, resulting in an ECIS50 value of approximately 12 microg/mL (ppm) after 25 h of exposure for a laminin coated gold surface. The effect of microcystin-LR on CHO cells probed by ECIS was inhibitory rather than cytotoxic, as confirmed by cell viability assays.

Reassessing culture media and critical metabolites that affect adenovirus production.

Adenovirus production is currently operated at low cell density because infection at high cell densities still results in reduced cell-specific productivity. To better understand nutrient limitation and inhibitory metabolites causing the reduction of specific yields at high cell densities, adenovirus production in HEK 293 cultures using NSFM 13 and CD 293 media were evaluated. For cultures using NSFM 13 medium, the cell-specific productivity decreased from 3,400 to 150 vp/cell (or 96% reduction) when the cell density at infection was increased from 1 to 3 x 10(6) cells/mL. In comparison, only 50% of reduction in the cell-specific productivity was observed under the same conditions for cultures using CD 293 medium. The effect of medium osmolality was found critical on viral production. Media were adjusted to an optimal osmolality of 290 mOsm/kg to facilitate comparison. Amino acids were not critical limiting factors. Potential limiting nutrients including vitamins, energy metabolites, bases and nucleotides, or inhibitory metabolites (lactate and ammonia) were supplemented to infected cultures to further investigate their effect on the adenovirus production. Accumulation of lactate and ammonia in a culture infected at 3 x 10(6) cells/mL contributed to about 20% reduction of the adenovirus production yield, whereas nutrient limitation appeared primarily responsible for the decline in the viral production when NSFM 13 medium was used. Overall, the results indicate that multiple factors contribute to limiting the specific production yield at cell densities beyond 1 x 10(6) cells/mL and underline the need to further investigate and develop media for better adenoviral vector productions.

Development of a suspension serum-free helper-dependent adenovirus production system and assessment of co-infection conditions.

Helper-dependent adenovirus (HDAd), deleted in all viral protein-coding sequences has been designed to reduce immune response and favor long-term expression of therapeutic genes in clinical programs. Its production requires co-infection of E1-complementing cells with helper adenovirus (HAd). Significant progresses have been made in the molecular design of HDAd, but large scale production remains a challenge. In this work, a scalable system for HDAd production is designed and evaluated focusing on the co-infection step. A human embryo kidney 293 (293) derived cell line, the 293SF/FLPe was generated to produce efficiently HDAd while restricting the packaging of HAd. This cell line was adapted to grow in suspension and in serum-free medium. Multiplicity of infection (MOI) of HDAd ranging from 0.1 to 50 was evaluated in presence of HAd at a MOI of 5. Optimal MOIs for HDAd amplification were found in the range of 5-10. HAd contamination was only 1%. These results were validated in a 3 L bioreactor under controlled operating conditions where a higher HDAd yield of 2.6 x 10(9) viral particles (VP)/mL or 3.5 x 10(8) infectious units (IU)/mL of HDAd was obtained.

Culture of HEK293-EBNA1 Cells for Production of Recombinant Proteins.

INTRODUCTIONFast and efficient production of recombinant proteins (r-proteins) remains a major challenge for the academic and biopharmaceutical communities. Pure r-proteins are often required in large amounts (hundreds of milligrams to gram quantities) when being developed as biotherapeutics, or in smaller quantities (milligrams) for high-throughput screening campaigns and structural or functional studies. Mammalian cells are often preferred over prokaryotic systems when expressing cDNAs of mammalian origin due to their superior capability to conduct elaborate post-translational modifications. Large-scale transfection of mammalian cells is now establishing itself as a "must-have" technology in the scientific community, as it allows the production of milligram to gram quantities of r-proteins within a few days after cDNA cloning into the appropriate expression vector. The HEK293 cell line stably expressing the Epstein-Barr virus nuclear antigen-1 (HEK293-EBNA1, or 293E) is the most commonly used cell line for large-scale transfection. When using expression vectors bearing the Epstein-Barr virus origin of replication, oriP (such as the pTT vector), a threefold improvement in r-protein yield is generally obtained over a similar non-oriP vector. This protocol describes a method for culturing HEK293-EBNA1 cells which will then be used to produce recombinant proteins.

Transfection of HEK293-EBNA1 Cells in Suspension with Linear PEI for Production of Recombinant Proteins.

INTRODUCTIONFast and efficient production of recombinant proteins (r-proteins) remains a major challenge for the academic and biopharmaceutical communities. Pure r-proteins are often required in large amounts (hundreds of milligrams to gram quantities) when being developed as biotherapeutics, or in smaller quantities (milligrams) for high-throughput screening campaigns and structural or functional studies. Mammalian cells are often preferred over prokaryotic systems when expressing cDNAs of mammalian origin due to their superior capability to conduct elaborate post-translational modifications. Large-scale transfection of mammalian cells is now establishing itself as a "must-have" technology in the scientific community, as it allows the production of milligram to gram quantities of r-proteins within a few days after cDNA cloning into the appropriate expression vector. Although calcium-mediated large-scale transfection is very effective, it is usually achieved in serum-containing medium under tightly controlled conditions that are difficult to achieve on a large scale. In contrast, polyethylenimine (PEI) is much easier to use: It binds to and precipitates DNA efficiently and the resulting DNA-PEI complexes are suitable for efficient transfection of mammalian cells. PEI has been used successfully on a large scale in serum-containing and serum-free cultures. In particular, the linear isoform of PEI is more effective for transfecting cells in suspension. This protocol describes the steps needed for successful transfection of HEK293 cells adapted to serum-supplemented or serum-free medium in suspension culture using linear PEI.

Transfection of Adherent HEK293-EBNA1 Cells in a Six-Well Plate with Branched PEI for Production of Recombinant Proteins.

INTRODUCTIONFast and efficient production of recombinant proteins (r-proteins) remains a major challenge for the academic and biopharmaceutical communities. Pure r-proteins are often required in large amounts (hundreds of milligrams to gram quantities) when being developed as biotherapeutics, or in smaller quantities (milligrams) for high-throughput screening campaigns and structural or functional studies. Mammalian cells are often preferred over prokaryotic systems when expressing cDNAs of mammalian origin due to their superior capability to conduct elaborate post-translational modifications. Large-scale transfection of mammalian cells is now establishing itself as a "must-have" technology in the scientific community, as it allows the production of milligram to gram quantities of r-proteins within a few days after cDNA cloning into the appropriate expression vector. Although calcium-mediated large-scale transfection is very effective, polyethylenimine (PEI) is much easier to use: It binds to and precipitates DNA efficiently and the resulting DNA-PEI complexes are suitable for efficient transfection of mammalian cells. In particular, the branched isoform of PEI works well for adherent cells, as it promotes their attachment to the plastic surface. It is thus very useful in experiments requiring multiple medium exchanges or washing steps following transfection. Also, when used in conjunction with six-well CellBIND plates, branched PEI can be used to adhere transfected cells when establishing stable cell lines. This protocol describes the steps needed for successful transfection of HEK293 cells adapted to serum-supplemented or serum-free medium in adherent culture using branched PEI.

Transfection of HEK293-EBNA1 Cells in Suspension with 293fectin for Production of Recombinant Proteins.

INTRODUCTIONFast and efficient production of recombinant proteins (r-proteins) remains a major challenge for the academic and biopharmaceutical communities. Pure r-proteins are often required in large amounts (hundreds of milligrams to gram quantities) when being developed as biotherapeutics, or in smaller quantities (milligrams) for high-throughput screening campaigns and structural or functional studies. Mammalian cells are often preferred over prokaryotic systems when expressing cDNAs of mammalian origin, due to their superior capability to conduct elaborate post-translational modifications. Large-scale transfection of mammalian cells is now establishing itself as a "must-have" technology in the scientific community, as it allows the production of milligram to gram quantities of r-proteins within a few days after cDNA cloning into the appropriate expression vector. Although calcium-mediated large-scale transfection is very effective, other methods suitable for efficient transfection of mammalian cells are easier to use. This protocol describes the steps needed for successful transfection of 293-6E cells in suspension culture in serum-free medium using 293fectin.

Purification of his-tagged proteins using fractogel-cobalt.

INTRODUCTIONFast and efficient production of recombinant proteins (r-proteins) remains a major challenge for the academic and biopharmaceutical communities. Such proteins often need to be as pure as possible before any characterization study can begin. Although many types of protein tag are available, histidine is the most popular. Although small-scale immobilized metal-affinity column (IMAC) purification of such proteins (e.g., <500 mL of culture medium) can easily be achieved using gravity chromatography columns, larger volumes can be processed with the aid of automated chromatography systems. This protocol describes an IMAC purification technique for secreted proteins using a cobalt-loaded resin. Preliminary small-scale trials using this technique can be used to determine the production scale that will be needed to provide enough pure material for a given study.